U.S. patent number 3,881,034 [Application Number 05/170,032] was granted by the patent office on 1975-04-29 for reconstituted egg product and method of preparing.
This patent grant is currently assigned to VioBin Corporation. Invention is credited to Ezra Levin.
United States Patent |
3,881,034 |
Levin |
* April 29, 1975 |
**Please see images for:
( Certificate of Correction ) ** |
Reconstituted egg product and method of preparing
Abstract
A stable dried egg powder containing a reduced amount of
cholesterol is made by removing the water and fat from whole raw
eggs in a body of solvent at a moderate temperature below levels
which would tend to cook the raw egg. The water is removed by
distillation as an azeotropic mixture of a solvent and water; the
fat is extracted into the solvent, the solvent drained off or
filtered and further removed, except for traces, by vacuum
distillation at a low temperature, an antioxidant is preferably
added, water is added to the dried product, and if desired a
portion of the egg fat or other additives also added, the mixture
homogenized and then dried.
Inventors: |
Levin; Ezra (Champaign,
IL) |
Assignee: |
VioBin Corporation (Monticello,
IL)
|
[*] Notice: |
The portion of the term of this patent
subsequent to September 21, 1988 has been disclaimed. |
Family
ID: |
26865622 |
Appl.
No.: |
05/170,032 |
Filed: |
August 9, 1971 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
Issue Date |
|
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702174 |
Feb 1, 1968 |
3607304 |
|
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Current U.S.
Class: |
426/541; 426/424;
426/429; 426/580; 426/614; 426/456; 426/603 |
Current CPC
Class: |
A23B
5/0255 (20130101); A23L 15/00 (20160801); A23V
2002/00 (20130101); A23V 2002/00 (20130101); A23V
2200/10 (20130101); A23V 2200/3262 (20130101); A23V
2300/14 (20130101) |
Current International
Class: |
A23L
1/32 (20060101); A23B 5/00 (20060101); A23B
5/025 (20060101); A23l 001/32 (); A23b
005/02 () |
Field of
Search: |
;99/113,208
;426/211,196,178,348,148,429,480,328 |
References Cited
[Referenced By]
U.S. Patent Documents
Foreign Patent Documents
Primary Examiner: Jones; Raymond N.
Attorney, Agent or Firm: Burmeister, York, Palmatier Hamby
& Jones
Parent Case Text
This application is a continuation-in-part of my copending
application, Ser. No. 702,174, filed Feb. 1, 1968 now U.S. Pat. No.
3,607,304.
Claims
I claim:
1. A dehydrated egg powder, said powder being substantially free of
water, said powder containing less than 5% free egg fat by weight,
and said powder containing between 10 and 100 parts per million of
fat solvent, and said powder containing an antioxidant.
2. A process of producing a nutritious egg product which comprises
the steps of
a. mixing raw eggs with a body or organic liquid fat solvent
capable of forming an azeotrope with water and which is nontoxic to
humans at levels of below 100 parts per million.
b. heating the body of solvent and eggs to a temperature of below
the coagulation temperature of the eggs to cause vapor of azeotrope
formed by the solvent and water from the eggs to boil off from the
solvent body, and extracting the dehydrated egg product so obtained
with said organic liquid fat solvent,
c. removing the fat containing solvent from the egg product to
obtain a substantially dehydrated and fat-free egg product,
d. thereafter adding water to said product in an amount sufficient
to form a flowable mixture and
e. thereafter drying said product to obtain a dry, substantially
solvent-free egg product.
3. A process according to claim 2 in which a fat antioxidant is
introduced into the product before drying said product.
4. A process according to claim 2 in which the organic fat solvent
is a chlorinated hydrocarbon.
5. A process according to claim 2 in which the organic fat solvent
is ethylene dichloride.
6. A process in accordance with claim 5 in which the process of
removing solvent is carried out so as to retain from 60-100 parts
per million of ethylene dichloride in the final product.
7. A process in accordance with claim 2 wherein egg fat in
substantially lesser proportion than that present in the original
eggs is introduced into the dry fat-free egg product after the
extraction step and prior to final drying.
8. A process in accordance with claim 7 in which the egg fat is
homogenized with the water and dry egg product and then the
homogenized mixture dried.
9. A process in accordance with claim 2 in which the removed egg
fat is replaced by mixing a cholesterol-free edible fat or oil with
the water and fat-free egg product prior to final drying.
10. A process in accordance with claim 9 in which the cholesterol
free fat or oil contains a flavoring agent.
11. A process according to claim 9 wherein the fat is
margarine.
12. A process according to claim 2 in which butter is mixed with
the water-free egg product prior to final drying.
13. A process according to claim 2 in which the organic fat solvent
is heptane.
14. A process according to claim 2 in which the organic fat solvent
is hexane.
15. A process in accordance with claim 9 wherein the fat is corn
oil.
16. In the process of producing a substantially water-free,
nutritious egg product in which raw eggs are mixed with an organic
liquid fat solvent which forms an azeotrope with water, the water
removed by distilling off the solvent-water azeotrope, and the fat
of the egg extracted with an organic liquid fat solvent to obtain a
substantially water-free egg product containing at least trace
amounts of organic liquid fat solvent, the improvement which
comprises mixing said water-free egg product with water and
evaporating water and solvent from said egg product and water
mixture so as to obtain a substantially dry and substantially
solventfree egg product.
17. A process according to claim 16 in which the egg product and
water are homogenized before final drying.
18. A process according to claim 16 in which the egg product and
water are homogenized with added edible fat before final
drying.
19. A process for removing fat solvent from dehydrated and defatted
egg containing fat solvent which comprises homogenizing said egg
product in water, and drying said homogenized mixture while
maintaining said mixture below the coagulation temperature of the
egg.
20. The process according to claim 19 in which the fat solvent is a
water immiscible liquid.
21. The process according to claim 19 in which the fat solvent is
ethylene dichloride.
Description
The invention relates to a dried egg product and more particularly
to an improvement in dried egg powder, and process of making
it.
An object of this invention is to provide a dried powdered egg
product which does not become rancid and which does not undergo the
so-called browning reaction which, so far as we know, occurs in
spray dried egg products heretofore made.
Another object is to provide a dried powdered egg product free of
or containing a reduced amount of cholesterol.
A further object is to provide a dried egg product in which all or
a part of the egg fat normally present in eggs is replaced by only
a portion of the egg fat, such as one-quarter, or replaced by
margarine, butter or other edible fats and oils containing
desirable flavors, such as butter flavor, bacon flavor or maple,
smoke or fruit flavors.
Another object is to provide a reconstituted egg powder of good
solubility and desirable taste.
A further object is to provide an improved process for dehydrating
and defatting whole eggs, and stabilizing said product.
Another object is to provide an improved process for desolventizing
eggs dehydrated by an azeotropic distillation process.
Other objects and advantages will become apparent as the following
detailed description progresses, reference being had to the
accompanying drawing showing a flow sheet of the process.
In accordance with this invention the dried egg product of the
invention is made by removing the egg shells, mixing, preferably by
homogenizing, raw whole liquid eggs with an organic solvent for the
egg fat which forms an azeotrope with water, removing the water by
distilling off azeotrope at below the coagulation temperature of
the egg, i.e., below 140.degree.F and preferably below 100.degree.F
and, if necessary, under reduced pressure, extracting the
dehydrated egg product with fat solvent, draining or filtering off
excess solvent and preferably vacuum drying the remaining solid
product to remove all but trace amounts of solvent, thereby
obtaining a dried fat-free and cholesterol-free egg product. This
product is then mixed with water and homogenized, and then dried.
The resulting product has high solubility and the fat solvent is
reduced to a value of below 100 ppm. However for extra high insect
resistance and freedom from Salmonella infection solvents such as
ethylene dichloride and like chlorinated hydrocarbon solvents of
from 60-100 ppm may be retained in the dried egg product. The term
"fat-free" is used herein to refer to a product having less than
five percent free fat by weight. There is also bound fat in the
product, but the cholestrol is substantially in the free fat.
The presence of low levels of residual fat make it desirable to add
small but effective and nontoxic levels of a fat antioxidant to the
egg product before homogenizing and spray drying. It may be added
to the boiling body of fat organic solvent as described in
application Ser. No. 702,174, or elsewhere in the process. Such
antioxidants, for example, may be butylated hydroxy toluene (BHT),
butylated hydroxy anisole (BHA), propyl gallate, normal
diguaiaretic acid (NDGA), or other antioxidants suitable for edible
fats. The use of antioxidants in this azeotropic fat solvent
process involving a drying step gives an exceptional degree of
stability since it prevents the rancidity.
In another embodiment of the invention the egg fat that has been
removed by the extraction process is partly replaced by the
addition of egg fat to make a low cholesterol egg with good flavor.
It has been found that replacement of between 15 per cent to 50 per
cent of the original fat of the egg, for example 25 per cent, gives
a highly satisfactory balance of low cholesterol and good flavor.
Further, the invention contemplates replacing all of the original
egg fat to produce a whole egg powder of improved stability.
Egg fat from which the cholesterol has been removed may also be
used to partially or completely replace the extracted egg fat of
the process.
In this process the replacement egg fat may suitably be added to
the dehydrated egg after the azeotropic distillation and draining
or filtering of the fat solvent, such as, for example, to the
mixture of dried defatted egg and water, after which the mixture is
homogenized and dried.
Instead of adding egg fat to the fat-free dried egg, the egg fat
may be only partially removed by extraction and draining so that a
portion of the egg fat remains with the solvent. The solvent is
then vacuum distilled away, except the minor amount which is
difficult to remove by this process, and the dried egg product
containing the egg fat left in the product is then mixed with
water, homogenized and dried as for the case where a portion of egg
fat is added to the fat free egg.
In another embodiment of the invention a reconstituted filled egg
powder is obtained. In this process, instead of replacing the
removed egg fat with a lesser amount of egg fat, it is replaced
with various other edible materials, especially cholesterol-free
edible fats and oils and flavoring compounds with or without fat or
oils. For example, the egg oil is replaced by butter, corn oil,
coconut oil, soybean oil, coconut oil flavored with butter flavor,
margarine, cottonseed oil containing butter flavor, bacon-flavored
fat. Desirable flavors such as maple, fruit flavors with or without
fat may be used. The process used is preferably that described for
incorporating a reduced amount of egg fat and the products obtained
are of like stability and solubility, and very low solvent content.
An antioxidant is preferably added to any edible oils added to the
product.
It is preferred to introduce the raw egg into the heated body of
fat organic solvent as an intimate mixture of the liquid egg and
the same fat organic solvent. In particular, the raw egg is
preferably emulsified in a fat organic solvent with the aid of a
conventional homogenizer, such as that provided by the
Cherry-Burrell Corporation. Different proportions of egg and fat
organic solvents may be used to prepare the emulsified mixture but
generally an excess volume of solvent is preferred, such as about 4
volumes of solvent to about 1 volume of raw egg. The emulsified egg
fat solvent mixture may then be below the surface of the heated
body of fat solvent heated at moderate temperature levels.
Practitioners will appreciate that the body of fat organic solvent
will be heated at the moderate temperature levels under decreased
pressure so that the fat organic solvent boils at the reduced
temperature and thereby forms an azeotrope of the water in the raw
egg and the fat organic solvent. The pressure level is applied in a
pressure vessel in the recognized manner of the art to attain the
formation of the azeotrope at its selected and desired temperature
level. The emulsified egg and solvent mixture may also be
introduced in an atomized form by delivering the emulsified mixture
under pressure through spray jets underneath the surface of the
body of boiling fat solvent.
Various fat organic solvents may be used which can form an
azeotrope in water, and many types of such solvents are described
in the foregoing U.S. Pat No. 2,503,313. In general, halogenated
hydrocarbons are preferred such as perchlorethylene,
trichlorethylene and, particularly, ethylene dichloride. Alcohol
may also be used.
The following examples are presented merely to illustrate ways to
practice the invention. Such examples should not be construed,
however, as representing the only way in which the improved egg
product may be prepared and evaluated.
EXAMPLE 1
Egg Product Preparation by Azeotropic Distillation with Ethylene
Dichloride
One volume of raw whole egg in liquid form is mixed with 4 volumes
of ethylene dichloride in a Cherry-Burrell homogenizer, and the
emulsified mixture is then introduced into a pressure vessel as a
fine spray below the level of the surface of a boiling body of
ethylene dichloride maintained at a temperature of no more than
40.degree.C, viz. 35.degree.C, and at a pressure of about 215 mm of
mercury.
An azeotrope of solvent and water is removed by distillation until
substantially all the water from the raw egg is withdrawn. The
temperature of the egg solvent mixture is maintained below about
40.degree.C throughout the distillation processing, and completion
of the distillation process is indicated by an increase in the
boiling temperature of the slurry of solvent, fat and egg solids
from the boiling point of the azeotrope to the boiling point of the
solvent. After substantial dehydration, the ethylene dichloride is
removed by draining through a screen opening in the vessel and
fresh solvent is added to the product which has been dried of
water. The mixture is stirred and the solvent is again removed by
draining through the opening in the vessel.
Two one-hundredths of one per cent by weight of fat present of
butylated hydroxy toluene (BHT) was mixed with the drained egg
product and 5 volumes of water added to give a flowable
mixture.
This mixture is then homogenized in a conventional homogenizer,
such as that provided by the Cherry-Burrell Corporation.
The homogenized composition is then dried in a conventional dryer.
The homogenized composition is at all times maintained at a
temperature below the coagulating temperature of egg. i.e., a
temperature of 40.degree.C and preferably 35.degree.C. Conventional
drying equipment may be used either with or without vacuum.
The product obtained is a dry, stable egg powder, substantially fat
free and substantially free of cholesterol, i.e. the free fat
content of the product has been reduced to about one per cent by
weight with a corresponding reduction in cholesterol. It has trace
levels of ethylene dichloride intimately contacted with the
individual particles to such a degree that the ethylene dichloride
content of the particles is less than 100 ppm.
EXAMPLE 2
Preparation of Egg Product by Azetropic Distillation with Ethylene
Dichloride
The process steps of Example 1 are essentially followed in that the
emulfisifed mixture of raw egg and ethylene dichloride is delivered
as a spray into the body of boiling ethylene dichloride at a point
just below the surface. The pressure in the closed pressure heating
vessel is about 215 mm of mercury. An azeotrope of solvent and
water is removed by distillation until substantially all the water
from the raw egg is withdrawn. The temperature of the egg solvent
mixture is maintained below about 40.degree.C throughout the
distillation processing. After substantial dehydration, the
ethylene dichloride, containing the fat, is removed by draining
through a screen opening in the vessel and fresh solvent is added
to the water-dried product. The mixture is stirred and the solvent
is again removed by draining through the opening in the vessel.
The process of Example 1 is then varied, however, in that the
drained egg product was then dried in a vacuum dryer at 200 mm of
mercury and 30.degree.C for three hours.
The dried product was mixed with water, homogenized and dried as in
Example 1.
The product was the same as in Example 1, except the product
contained less ethylene dichloride, the amount varying depending
upon the time of vacuum drying, and time and temperature of the
final drying step, as low as 10 ppm and less being obtained.
EXAMPLE 3
The process of Example 2 was repeated except that the ethylene
dichloride from the extractor which contains the egg fat was vacuum
distilled to remove the solvent and obtain the egg fat, and egg fat
in amount such as to bring the dried fat-free egg to 25 per cent of
its normal level was added to the mixture of dried fat-free egg
with water, as shown in the flow sheet of the accompanying drawing,
and the mixture homogenized and dried as described for the fat-free
product of Examples 1 and 2.
The powdered egg product obtained had very good flavor,
corresponding closely to that of fat-containing egg, and had less
than 25 per cent of the cholesterol of a normal egg. It was stable
and of good solubility.
EXAMPLE 4
The process of Example 3 was repeated except that instead of adding
25 per cent of normal egg fat, there was added vegetable margarine
(free of cholesterol) in an amount equal to that of the normal
amount of egg fat, so that the original egg fat of the whole egg
was replaced with margarine, thus giving cholesterol-free powdered
egg product containing fat in amount normally found in eggs, and of
good flavor.
Similarly to Example 4, other fats and oils may be used, such as
corn oil, coconut oil, or soybean oil, preferably containing a
small and flavoring amount of a flavoring agent, such as butter
flavor or the like. Also, butter or bacon flavored fat may be used
to replace the egg fat. Maple, fruit flavors and the like may
readily be incorporated. When adding fat to the product, such as
corn oil, soybean oil, coconut oil or margarine, it is preferable
to add an antioxidant to the oil prior to introducing the oil into
the process. For example, .02 per cent by weight of the oil
butylated hydroxy toluene (BHT) should be added to corn oil or
soybean oil or coconut oil prior to adding the oil to the product.
The additives are preferably incorporated by adding to the dried
fat-free egg, mixing with water and homogenizing. However, they
could be added anytime after draining off the fat containing
solvent, but a more uniform product is obtained by adding the fats
and other additives before homogenizing.
EXAMPLE 5
The process of Example 1 was repeated utilizing hexane as the
solvent in place of ethylene dichloride. The temperature of the
egg-hexane mixture is maintained below about 40.degree.C throughout
the distillation processing by performing the distillation step
under a partial vacuum, the temperature of the product being
preferably maintained at about 35.degree.C.
EXAMPLE 6
The process steps of Example 5 are followed in that emulsified
mixture of the raw egg and hexane is delivered as a spray into the
body of boiling hexane at a point just below the surface thereof.
An azeotrope of solvent and water is removed by distillation until
substantially all the water from the raw egg is withdrawn. The
temperature of the egg solvent mixture is maintained at a
temperature of about 35.degree.C throughout the distillation
process, and in all events less than 40.20 C. After substantial
dehydration, the hexane containing the fat is removed by draining
through a screen opening in the vessel and fresh solvent is added
to the water dried product. The mixture is stirred and the solvent
is again removed by draining through the opening in the vessel.
The process of Example 5 is then varied in that the drained egg
product was then dried in a vacuum dryer at 200 mm of mercury and
30.degree.C for 3 hours.
The dried product was mixed with water, homogenized and dried as in
Example 5. The end product is similar to that obtained in Example 5
except the amount of hexane remaining in the product is
substantially reduced, to the order of 10 parts per million.
EXAMPLE 7
The process of Example 6 was repeated except that corn oil in an
amount equal to the egg fat removed from the product was added to
the mixture of dried fat free egg with water, as shown in a sheet
of the accompanying drawings, and the mixture homogenized and dried
as described for the fat-free product of Examples 5 and 6.
EXAMPLE 8
The process of Example 7 is followed except that the solvent was
heptane.
The egg product prepared according to the teachings of Examples 1-8
is analyzed to determine its protein and lipoprotein by the methods
described in A.O.A.C. Methods of Analysis, 10th Ed.
The Food and Drug bacteriological method is employed to determine
any salmonella infection. The cholesterol content is determined by
the method described in Anal. Chem., Vol. 22, page 1,210 (1950).
The presence of Salmonella infection is studied by the method
described in the Bacteriological Analytical Manual, Food and Drug
Administration, 1966.
The protein content of the fat free product, i.e., (the product
prepared by Examples 1 or 2) was found to be about 75 percent by
weight and the lipoprotein content about 9 percent by weight. The
protein content quantity of egg products prepared by the prior art
method of spray drying was found to have a protein quantity of 45
per cent or substantially lower than the protein quantity of the
egg product of the present invention. The egg product of Examples
1, 2, 4, 5, 6, 7 and 8 was substantially free of cholesterol as
compared to the original cholesterol levels and the cholesterol
levels of the prior art spray dried egg products. The egg product
of the invention is free of any Salmonella infection.
Protein Efficiency Ratio of Egg Product
The egg product prepared by the method of Examples 1-8 is subjected
to Derse Assay for 4 weeks and compared with the recognized
standard of casein (milk protein). The casein had a P.E.R. or
protein efficiency ratio of 2.80 whereas the egg products of this
invention had a P.E.R. or protein efficiency ratio of 4.03.
The improved egg product of this invention permits the product to
be provided to the consumer in a packaged form because of its
indefinite shelf-life which results in a stability heretofore
unknown for dried egg products. It is recognized that the prior art
egg products prepared by spray drying have limited stability in
storage at room temperature.
It will also be appreciated that the substantial removal of
cholesterol, up to about 96 per cent, or the substantial reduction
of cholesterol makes the product attractive to those many consumers
who diligently attempt to avoid cholesterol in their diets.
The elimination of the problem of pathogenic organisms, namely,
Salmonella, is a marked improvement because prior art egg products
prepared by spray drying require pasteurization to eliminate this
problem. This pasteurization step is cumbersome and uneconomical
because it is a sensitive procedure. If pasteurization exceeds a
predetermined upward temperature level, coagulation of protein
occurs which will frustrate attempts to dissolve the powdered egg
product in water prior to cooking. If a lower pasteurization level
is not attained, then the pathogenic organism is not destroyed.
Such an added procedure is never required with the egg product of
the present invention because Salmonella infection is entirely
eliminated by the presence of the fat organic solvent, particularly
a halogenated hydrocarbon solvent.
Not only are the trace levels of ethylene dichloride nontoxic, but
the ethylene dichloride tends to become volatilized upon cooking of
the egg product. The instant egg product undergoes ready admixture
with added water and cooks to a homogenous and good appearance. The
improved resistance to insect infestation, imparts additional
advantages relative to the feature of storage, since the likelihood
of this potential hazard is reduced.
The egg oil, which is contained in the miscella, drained from the
egg solids after evaporation of the watersolvent azeotrope, is in
itself a valuable product. As indicated in the flow sheet, the
solvent is vacuum distilled from the egg oil and the egg oil
collected in a storage tank.
The egg oil will contain the phosphatides present in the egg if the
extraction is performed with a polar or partial polar solvent, such
as ethylene dichloride, which is not the case of egg oil extracted
with a non-polar solvent such as heptane or hexane. Egg oil
containing the phosphatides of the egg is a particularly valuable
product, since it is an emulsifying agent and suitable for use in
cosmetics. Egg oil produced in this manner is made stable by
addition of an antioxidant. For example, 0.02 per cent butylated
hydroxytoluene (BHT) by weight of the oil is added to the egg oil
and produces a stable product. While the phosphatides are valuable
constituents of egg oil, they are undesirable in the egg solids
since they adversely affect stability and taste.
Egg powder produced in accordance with this invention is in the raw
state, that is, the product retains the water soluable coaguables
and the enzymes of raw egg.
The invention may now be practiced in the various ways which will
occur to practitioners, and all such practice is intended to be a
part of the present invention provided it comes within the terms of
the following claims as given further meaning by the language of
the preceding specification.
* * * * *